Search Images Maps Play YouTube News Gmail Drive More »
Sign in
Screen reader users: click this link for accessible mode. Accessible mode has the same essential features but works better with your reader.

Patents

  1. Advanced Patent Search
Publication numberUS8046934 B2
Publication typeGrant
Application numberUS 12/162,030
PCT numberPCT/EP2007/050693
Publication dateNov 1, 2011
Filing dateJan 24, 2007
Priority dateJan 25, 2006
Also published asEP1977177A1, EP1977179A1, US20090007453, US20090031581, WO2007085617A1, WO2007085618A1
Publication number12162030, 162030, PCT/2007/50693, PCT/EP/2007/050693, PCT/EP/2007/50693, PCT/EP/7/050693, PCT/EP/7/50693, PCT/EP2007/050693, PCT/EP2007/50693, PCT/EP2007050693, PCT/EP200750693, PCT/EP7/050693, PCT/EP7/50693, PCT/EP7050693, PCT/EP750693, US 8046934 B2, US 8046934B2, US-B2-8046934, US8046934 B2, US8046934B2
InventorsPatrick Lenoir
Original AssigneeNv Bekaert Sa, Bekaert Combustion Technology B.V.
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Convective system for a dryer installation
US 8046934 B2
Abstract
The present invention concerns a convective system for a dryer installation for a passing web, more particularly paper. The convective system 7 is an assembly of an exterior casing 13 for suction of combustion products with opening 14 towards the web, with a first 15 and second 16 suction ducts sucking the combustion products into the convective system 7. The combustion products coming from the first suction duct 15 are guided through the exterior casing 13 to a mixing and blowing device 17. Cold air 18 is mixed in this mixing and blowing device 17 with the combustion products 19, resulting in a gas mixture with lower temperature 20. The convective system 7 also has an internal casing 21 inside the external casing 13. This internal casing 21 has at least one opening towards the web 22 and has also openings 34 allowing gas flow from the mixing device 17 to the internal casing 21 of said gas mixture 20. Under the internal casing 21, there is also a blowing duct 23. The second suction duct 16 is also arranged under this internal casing 21 thereby extracting a second flow of combustion products 24 into the internal casing 21. This second flow 24 of combustion products is then mixed with the gas mixture 20 coming from the mixing device 17, resulting in a mixture of gasses 25 with a temperature that is higher than the first gas mixture 20 and higher than e.g. 350° C. or 370° C., more preferably 390° C. or 410° C., even more preferably 420° C., 450° C. or 500° C. These hot gasses 25 are then blown to the drying web by the blowing duct 23 of the internal casing 21.
Images(5)
Previous page
Next page
Claims(13)
1. A convective system for a dryer installation arranged transversally with respect to a web to be dried,
said convective system comprising
an exterior casing for suction of combustion products with opening towards the web
a first and second suction ducts and sucking said combustion products into said convective system
said first suction duct sucking said combustion products into said exterior casing
a mixing and blowing device for re-use of said combustion products, thereby mixing cold air with said combustion products resulting in a gas mixture with lower temperature
an internal casing inside said external casing with at least one opening towards the web
said internal casing having openings allowing gas flow from external casing to internal casing of said gas mixture
a blowing duct under said internal casing wherein
said second suction duct is also arranged under said internal casing
said second suction duct extracting a second flow of combustion products into said internal casing
said second flow of combustion products consequently being mixed with said gas mixture with lower temperature resulting in a mixture of gasses with a temperature that is higher than said first gas mixture
said resulting mixture of gasses being blown to the drying web by said blowing duct.
2. A convective system according to claim 1, wherein the mixing and blowing device is a venturi.
3. A convective system according to claim 1, wherein the blowing duct is arranged between said first suction duct and said second suction duct.
4. A convective system according to claim 1, wherein said internal casing is designed in such a way as to provide a good air distribution.
5. A convective system according to claim 1, wherein the system also comprises an air pressure sensor in order to assure constant flotation effect on the web.
6. A convective system according to claim 1, wherein the system also comprises a temperature sensor.
7. A convective system according to claim 1, wherein said mixing and blowing device at least has one turbine of which the axis is substantially perpendicular to the web.
8. A convective system according to claim 1, wherein said mixing and blowing device at least has one turbine of which the axis is substantially parallel to the web.
9. A method for safeguarding a fan from contact with hot combustion gasses by using a system according to claim 1.
10. A method of re-using heated gasses to enhance the heat exchanging efficiency using the system according to claim 1.
11. A dryer installation for drying web, more particularly paper, said installation being provided for drying a maximum web width, said installation comprises gas-heated radiant elements for radiating said web, arranged according to at least one row stretching out in the transversal direction over the substantially entire maximum web width, said installation comprising at least one transversal convective system according to claim 1.
12. A dryer installation for drying web, more particularly paper, said installation being provided for drying a maximum web width, said installation comprises at least one burner assembly adapted to burn in blue flame mode for heating said web, arranged according to at least one row stretching out in the transversal direction over the substantially entire maximum web width, said installation comprising at least one transversal convective system according to claim 1.
13. Dryer installation according to claim 11, wherein said installation comprises at least two transversal convective systems arranged one after the other in the passing direction of the web and separated one from the other by at least one transversal row of heating elements.
Description
TECHNICAL FIELD

The present invention concerns a convective system for a dryer installation for a passing web, more particularly paper.

BACKGROUND ART

There exists e.g. according to FR-A-2771161 in the name of the applicant an installation having at least a web, gas-heated radiant elements arranged according to at least one row stretching out in the transversal direction of the web, substantially over its entire width, and, downstream at least one row of radiant elements, at least a transverse convective system equipped with suction and blowing devices to suck at least part of the combustion products produced by the radiant elements and to blow this part of the combustion products towards the web. The installation generally also has devices to extract the warm gasses resulting from the convective exchanges between the passing web and the combustion products.

The suction and blowing devices have a mixing device, such as e.g. a ventilator, that is, for several known reasons, shifted laterally at the outside of the web, in relation to the median longitudinal axis usually at a large, even extremely large, distance in relation to the width of the web. In that way, the ventilator has to laterally collect the combustion products that are initially divided over the entire width of the web, mix the combustion products and divide them again over the entire width of the web. Such a mixing entails an important consumption of energy.

In addition, such an installation has suction and blowing ducts that, at least in the transverse direction of the web, have an important size. These ducts dissipate thermal energy by radiation and convection. There is amongst other things aspiration of cold air that is cooling down the combustion products. Hence, the temperature of the combustion products blown on the web is considerably lower than the temperature of the combustion products generated by the radiant elements.

Such an installation, although functioning satisfactorily, thus implies a considerable consumption of mechanical energy and also a considerable loss of thermal energy, thus resulting in considerable investment and operating costs, and also occupies a large surface. An already improved system has been described in WO 2005/085729 in the name of the applicant resulting in a reduced consumption of mechanical energy and a reduced loss of thermal energy, lower investment and operation costs, and necessitating less space. This dryer installation is characterized by the fact that the suction and blowing devices of the convective system have at least one suction and blowing device installed opposite of the passing web in relation to corresponding suction and blowing ducts that at least stretch out in the transverse direction of the web, and arranged so as to suck and/or blow the said combustion products in such a way that the vector averages are optimized. The vectors are representing the respective trajectories of the different jets of sucked and/or blown combustion products. This optimization considerably reduces the trajectories of the jets of combustion products and the mechanical mixing energy needed to suck and blow the different jets of combustion products. These shorter trajectories of combustion products require shorter suction and blowing ducts and smaller dimensions corresponding to smaller surfaces that lead to considerably smaller losses of thermal energy by radiation and convection.

Likewise, the temperature difference between the sucked combustion products and the blown combustion products is substantially reduced, thereby increasing the efficiency.

In that way, the thermal transfers between the combustion products and the passing plane can be maximized, and it is also possible to obtain an extremely compact dryer installation in which the combustion products are blown at the highest possible temperature.

Although above described system has already improved the efficiency of the dryer installation to a large extent, there is still a major restriction to the system in that the mixing devices cannot withstand temperatures that are higher than e.g. 350° C., thereby limiting the temperature of the warm blown combustion products.

SUMMARY OF THE INVENTION

The objective of the present invention is to mitigate the restrictions of the known installations and to propose a convective system for a dryer installation having a more reduced consumption of mechanical energy and a more reduced loss of thermal energy and lower investment and operation costs. A further objective of the present invention is to accomplish an improvement within existing systems and within the existing dimensions. Still another objective of the present invention is to accomplish an improvement by means of simple measures.

According to a first aspect of the invention, there is provided a convective system for a dryer installation arranged transversely with respect to a web to be dried. The convective system is an assembly of an exterior casing for suction of combustion products with opening towards the web, with a first and second suction ducts sucking the combustion products into the convective system. The combustion products coming from the first suction duct are guided through the exterior casing to a mixing and blowing device. Cold air is mixed in this mixing and blowing device with the combustion products, resulting in a gas mixture with lower temperature.

The convective system also has an internal casing inside the external casing. This internal casing has at least one opening towards the web and has also openings allowing gas flow from the external casing to the internal casing of said gas mixture. Under the internal casing, there is also a blowing duct. The second suction duct is also arranged under this internal casing thereby extracting a second flow of combustion products into the internal casing. This second flow of combustion products is then mixed with the gas mixture with lower temperature coming from the mixing device, resulting in a mixture of gasses with a temperature that is higher than the first gas mixture and higher than e.g. 350° C., more preferably 400° C. or 450° C., even more preferably 500° C. These hot gasses are then blown to the drying web by the blowing duct of the internal casing.

Also according to the invention this improved convective system can be achieved by simple means, by applying an inner casing into the outer casing. It is clear that applying an inner casing can be done without difficulties, thus in a simple way.

Applying an inner casing can be realized both in a completely new convective system and in an existing convective system without changing drastically the dimensions.

This direct re-use of hot combustion products in the internal casing increases the temperature of the blown gasses resulting in a more efficient use of the heat produced by the dryer system and improving the efficiency of the heat exchange in the system.

According to an alternative version of the invention, the convective system is constructed with a mixing and blowing device being a venturi-system.

According to another version of the invention, the convective system is designed in such a way that the blowing duct is arranged between said first suction duct and said second suction duct.

A preferable embodiment of the invention provides a special design of the internal casing resulting in a good air distribution.

Another preferred embodiment of the invention provides in the system an air pressure sensor in order to assure constant flotation effect on the web to be dried. A temperature sensor can also be foreseen.

A preferred embodiment of the invention is the convective system wherein the mixing and blowing device at least has one turbine of which the axis is perpendicular to the web. Another version of the invention is the convective system wherein the mixing and blowing device at least has one turbine of which the axis is parallel to the web.

According to a second aspect, the invention provides a method for safeguarding a fan from contact with hot combustion gasses by using above described convective system.

According to a third aspect, the invention provides a method of re-using heated gasses to enhance the heat exchanging efficiency using the above described convective system.

Above described convective system can then be used in a dryer installation for drying a web, e.g. paper. The dryer installation is designed for drying a maximum web width and is composed of gas-heated radiant elements for radiating said web next to the convective system. The radiant elements are arranged in at least one row stretching out in the transversal direction over the substantially entire maximum web width. A further implementation of the invention is an installation which has at least two transverse convective systems arranged one after the other in the passing direction of the web and separated one from the other by at least one transverse row of gas-heated radiant elements.

In the same way can the above described convective system be used in a dryer installation based on a burner assembly, said dryer installation e.g. being of a flame drier type.

In an even more preferred embodiment of the invention the system of re-using the exhaust gases is set up in a cascade system, wherein the exhaust gasses coming directly from the heating assembly (e.g. burner system, gas-heated radiant elements) are sucked and blown to the web by a first convective system. The warm gasses which are then available at the second convective system are again sucked for re-use and re-blown thereby making further use of the available thermal energy which was created by the heating assembly. For example, first there is the heating assembly with temperatures over 1000° C. thereafter a first convective system which blows re-used exhaust gasses at 400° C. and thereafter a second convective system which blows gasses at 200° C. This further increases the drying efficiency of the system.

One can even consider putting one of above described installations on each side of the web to be dried.

BRIEF DESCRIPTION OF DRAWINGS

The invention will now be described into more detail with reference to the accompanying drawings wherein:

FIG. 1 is a schematic view of a dryer system

FIG. 2 is a cross-section of a convective system according to a plane B-B′ that stretches out in the longitudinal direction of a web and that is perpendicular to the direction of the movement of the web, showing the structure of the convective system;

FIG. 3 a is a cross-section of a convective system according to a plane B-B′ that stretches out in the longitudinal direction of a web and that is perpendicular to the direction of the movement of the web, showing the respective gas flows occurring in a first step of the convective system with respect to the moving direction of the web;

FIG. 3b is a cross-section of a convective system according to a plane B-B′ that stretches out in the longitudinal direction of a web and that is perpendicular to the direction of the movement of the web, showing the respective gas flows occurring in an alternative setup of the convective system with respect to the moving direction of the web;

FIG. 4 is a cross-section of a convective system according to a plane A-A′ that stretches out in the transverse direction of the web and that is perpendicular to the direction of the movement of the web;

FIG. 5 is a cross-sectional view of another realization method of the present invention;

FIG. 6 is a cross-sectional view of a dryer installation according to a first realization mode of the present invention;

FIG. 7 is a schematic cross-sectional view of a dryer installation according to another realization mode of the present invention;

FIG. 8 is a schematic cross-sectional view of a flame dryer installation according to an alternative realisation mode of the present invention.

REFERENCE LIST OF USED NUMBERS IN THE FIGURES

  • dryer installation 1
  • passing web 2
  • gas-heated radiant elements 3
  • one row of gas-heated radiant elements 4
  • transverse direction arrow 5
  • passing direction of the web 6
  • convective system 7
  • suction and blowing devices 8
  • devices to extract the warm gasses resulting from the convective thermal exchanges,
  • Arrow 9
  • gas supply tubes 10
  • combustion air supply tubes 11
  • air/gas alimentation 12
  • exterior casing 13
  • opening towards the web 14
  • first suction duct 15
  • second suction duct 16
  • a mixing and blowing device 17
  • Fresh cold air 18
  • combustion products 19
  • gas mixture with lower temperature 20
  • internal casing 21
  • opening in internal casing towards the web 22
  • blowing duct 23
  • a second flow of combustion products 24
  • mixture of gasses with t° higher than from (20) 25
  • extraction duct 26
  • cylindrical rotor 27
  • corresponding enclosed space for cylindrical rotor 28
  • axis of the rotor 29
  • turbine 30
  • axis of turbine 31
  • suction opening of turbine 32
  • tangential outlet opening of turbine 33
  • openings allowing gas flow from the mixing device 17 to the internal casing 34
  • burner assembly 35
DESCRIPTION OF THE PREFERRED EMBODIMENTS OF THE INVENTION

The present invention will be described with respect to particular embodiments and with reference to certain drawings but the invention is not limited thereto but only by the claims. The drawings described are only schematic and are non-limiting. In the drawings, the size of some of the elements may be exaggerated and not drawn on scale for illustrative purposes. The dimensions and the relative dimensions do not correspond to actual reductions to practice of the invention.

Furthermore, the terms first, second, third and the like in the description and in the claims, are used for distinguishing between similar elements and not necessarily for describing a sequence, either temporally, spatially, in ranking or in any other manner. It is to be understood that the terms so used are interchangeable under appropriate circumstances and that the embodiments of the invention described herein are capable of operation in other sequences than described or illustrated herein.

FIG. 1 represents a dryer installation 1 for a passing web 2, more particularly paper, e.g. for a web of coated paper that has been treated in a humid way and has to be dried without contact.

The installation 1 has at least the web 2 and the gas-heated radiant elements 3. The elements 3 are arranged according to at least one row 4 stretching out in the transversal direction 5 of the web 2. The row 4 substantially stretches over the entire maximum web width.

The installation 1 also has at least one convective system 7 downstream of at least one row 4 of radiant elements 3, referring to the direction of the passing of the web 6. The convective system includes suction and blowing devices 8. The devices 8 suck at least a part of the combustion products generated by the radiant elements 3 and blow those combustion products towards the web 2. The convective system also has devices 9 to extract the warm gasses resulting from the convective thermal exchanges between the passing web 2 and those combustion products.

The radiant elements 3 can be gas-heated radiant elements of whatever type, arranged in any possible way in relation to one another and in relation to gas supply tubes, and to combustion air supply tubes.

According to the present invention, the suction and blowing devices 8 include at least one mixing device 12 installed opposite of the passing web 2.

FIG. 2 represents a section of the convective system 7 according to a plane perpendicular to the web that stretches out in the longitudinal direction of the web (according to B-B′).

FIG. 3 a shows the respective gas flows in the convective system with a first suction duct 15 with respect to the moving direction of the web.

FIG. 3 b shows an alternative setup of the convective system with regard to the moving direction of the web.

Reference is made to FIG. 2 and FIG. 3A. The convective system 7 is an assembly of an exterior casing 13 for suction of combustion products with opening 14 towards the web, with a first 15 and second 16 suction ducts sucking the combustion products into the convective system 7. The combustion products coming from the first suction duct 15 are guided through the exterior casing 13 to a mixing and blowing device 17. Cold air 18 is mixed in this mixing and blowing device 17 with the combustion products 19, resulting in a gas mixture with lower temperature 20. The convective system 7 also has an internal casing 21 inside the external casing 13. This internal casing 21 has at least one opening towards the web 22 and has also openings 34 allowing gas flow from the mixing device 17 to the internal casing 21 of said gas mixture 20. Under the internal casing 21, there is also a blowing duct 23. The second suction duct 16 is also arranged under this internal casing 21 thereby extracting a second flow of combustion products 24 into the internal casing 21. This second flow 24 of combustion products is then mixed with the gas mixture 20 coming from the mixing device 17, resulting in a mixture of gasses 25 with a temperature that is higher than the first gas mixture 20 and higher than e.g. 350° C. or 370° C., more preferably 390° C. or 410° C., even more preferably 420° C., 450° C. or 500° C. These hot gasses 25 are then blown to the drying web by the blowing duct 23 of the internal casing 21. FIG. 3B depicts an alternative embodiment following the same principle as in FIG. 3A.

FIG. 4 is a cross-section, according to a plane perpendicular to the web 2 that stretches out in the transverse direction of the web (according to A-A′), of the convective system 7. The suction ducts 15 and 16 and blowing duct 23 stretch out over the total web width, but are not indicated in this figure. In order to achieve a good three-dimensional air distribution in the inner duct 21, the convective system 7 can preferably be designed as indicated in FIG. 4. The internal casing 21 comprises also an extraction duct 26 that is part of the devices 9. The extraction duct 26 extracts part of the warm gasses 25 and part of the combustion gasses 19. This extraction duct 26 is asymmetrically arranged in the convective system 7. In order to obtain a good air blowing distribution, the inner height of the internal casing 21 is also asymmetric and increases towards the extraction duct 26. The devices 9 are known extraction devices, e.g. a fan.

In the represented example, each turbine 30 has a centrifugal turbine wheel of which the suction opening 32 is connected to an upstream transverse suction duct 15 in relation to the web 2. The wheel is driven by an engine, as in any conventional fan.

The mixed gasses 20 are blown through two tangential outlet openings 33 substantially directly opposite to the transverse direction 5 of the web 2, and connected to two transversal blowing ducts 34.

FIG. 5 shows another preferred embodiment of the invention. Here, the mixing and blowing device of the convective system has at least one turbine of which the axis is parallel to the web. A cylindrical rotor 27 is installed at the interior side of the first external casing 13. Each cylindrical rotor 27 is installed inside a corresponding enclosed space 28 and has radial blades. Each cylindrical rotor 27 turns around a respective axis 29 parallel to the web 2 and substantially perpendicular to the passing direction 6 of the web 2.

In the represented example, the different rotors 27 are installed on the same pole driven by an engine.

Another preferred embodiment of the invention is a convective system 7 wherein the mixing and blowing device at least has one turbine of which the axis is perpendicular to the web, as in e.g. a fan. This axis can also be given other directions inclined in any possible direction in relation to the web, without leaving the scope of the present invention.

In the realization mode of FIGS. 6 and 7, each convective system 7 at least has one turbine 30 of which the axis 31 is substantially perpendicular to the web 2.

Each convective system can have a fresh air inlet opening, along a lateral edge of the web 2, for instance in the right-hand side of FIG. 4. This fresh air inlet is advantageously closed off by a valve to allow the entrance of ambient temperature air inside the suction duct 15 in order to dilute the combustion products and thus limit the temperature of the combustion products sucked by turbine 30, if necessary.

In addition, each convective system 7 also has an extraction opening as described above.

Another preferred embodiment of the invention is a convective system wherein the mixing device 12 is an organ adapted to blow air under pressure through the openings 33 of FIG. 4. This creates a venturi effect which sucks at least part of the combustion products through the suction duct 15 and blows them in the internal casing 21.

Obviously, the present invention is not limited to the realization modes described above, and many changes and modifications can be made to these realization modes without leaving the scope of the present invention.

One can of course use any mixing device adapted to suck and blow the combustion products, and arrange these mixing devices and the corresponding suction and blowing ducts in any known way.

The afore-described mixing devices can also be arranged in a different way than the ways described above.

These mixing devices and the corresponding transversal convective systems can be linked to gas-heated radiant elements of any type, and these radiant elements can be arranged in any possible way.

These mixing devices and the corresponding transversal convective systems can in the same way be linked to gas-heated burners elements of any type, e.g. a blue flame burner, and these burner elements can be arranged in any possible way.

As schematized in FIGS. 1, 6 and 7, one can foresee at least two convective systems 7 according to the present invention, arranged one after the other in the passing direction 6 of the web 2 and separated from one another by at least one transversal row 4 of gas-heated radiant elements. According to FIG. 7, an arrangement of such radiant elements and convective systems can be put on each side of the web to be dried.

Obviously, the devices of the invention described above, the suction ducts 15 and 16 and the blowing duct 23, the mixing devices 30, the exterior 13 and interior casing 21, etc. are designed and arranged in a known way so that they can endure durably and reliably the high temperatures of the sucked and/or blown combustion products.

As schematised in FIG. 8 one can foresee at least two convective systems according to the present invention, arranged one after the other in the passing direction of the web 2, in a drier installation. In this so called cascade system, the exhaust gases are coming directly from a burner assembly, and are sucked by the convective system whereafter these hot gasses are blown to the web for re-use, by the blowing duct. The warm gasses which are then available at the convective system can again be sucked for re-use and reblown thereby making further use of the available thermal energy which was created by the burner assembly. For example, first there is the burner assembly with temperatures over 1000° C. thereafter a first convective system which blows reused exhaust gasses at 400° C. and thereafter a second convective system which blows gasses at 200° C. This cascade system of re-using the created hot-air flows can also be used in other drying systems, e.g. in combination with IR-dryers.

Obviously, it is also possible to foresee, in addition, thermal insulation devices and/or traditional cooling-down devices known to protect certain specific devices, such as e.g. an electrical engine.

We have thus described and represented a convective system for use in a dryer installation designed and arranged to limit as much as possible thermal losses in order to maintain the high energy potential of these combustion products and thus allow an excellent return of the convective thermal exchanges between the web and the sucked and blown combustion products.

In addition to the important improvement of the thermal exchanges between the combustion products and the web, the mechanical energy needed to suck and blow these combustion products is also considerably reduced.

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US2668700 *May 25, 1949Feb 9, 1954Zimmerman Richard GDrier for printing presses
US2987305 *May 31, 1957Jun 6, 1961J V Calhoun CompanyMethods of and apparatus for generating and transferring heat
US3096162 *Feb 18, 1959Jul 2, 1963Spooner Dryer & Eng Co LtdGaseous restraint of conveyed articles
US3231985 *Jan 15, 1962Feb 1, 1966Hupp CorpHeating, drying and curing apparatus and methods
US3416237 *Dec 21, 1966Dec 17, 1968Paper Board Printing Res AssMethod and apparatus for drying flexible material such as paper and board formed from cellulosic fibrous material
US3590495 *May 2, 1969Jul 6, 1971Goodyear Tire & RubberDryer or heater with shielding means
US3643342 *Aug 17, 1970Feb 22, 1972Goodyear Tire & RubberDryer or heater with shielding means
US3744963 *Nov 19, 1971Jul 10, 1973Nat Lumberman S Bank & Trust CHeat treatment
US4094627 *Sep 15, 1975Jun 13, 1978Milton Jr Clare LOven system
US4290269 *Oct 9, 1979Sep 22, 1981Modo-Chemetics AbProcess for the efficient conversion of water-containing organic materials as fuels into energy
US4622758 *Sep 11, 1985Nov 18, 1986Oy Tampella AbMethod of and a device for drying a paper web or the like
US4726124 *Feb 12, 1987Feb 23, 1988A. Monforts Gmbh & Co.Textile machine having continuous convective heat treatment
US5069801 *Feb 26, 1990Dec 3, 1991Bio Gro Systems, IncorporatedOdorless conversion to fertilizer
US5105558 *Mar 28, 1991Apr 21, 1992Curry Donald PApparatus and process for drying cellulosic and textile substances with superheated steam
US6085437 *Jul 1, 1998Jul 11, 2000The Procter & Gamble CompanyWater-removing apparatus for papermaking process
US6088930Nov 11, 1998Jul 18, 2000Solaronics Process SaConvection-radiation system for heat treatment of a continuous strip
US6264791 *Oct 25, 1999Jul 24, 2001Kimberly-Clark Worldwide, Inc.Flash curing of fibrous webs treated with polymeric reactive compounds
US6308436 *Jul 1, 1998Oct 30, 2001The Procter & Gamble CompanyProcess for removing water from fibrous web using oscillatory flow-reversing air or gas
US6393719 *May 3, 2000May 28, 2002The Procter & Gamble CompanyProcess and apparatus for removing water from fibrous web using oscillatory flow-reversing air or gas
US6432267 *Dec 8, 2000Aug 13, 2002Georgia-Pacific CorporationWet crepe, impingement-air dry process for making absorbent sheet
US6470597 *May 3, 2000Oct 29, 2002Institute Of Paper Science And Technology, Inc.Process and apparatus for removing water from materials using oscillatory flow-reversing gaseous media
US6511015Mar 17, 2000Jan 28, 2003Metso Paper, Inc.Method and apparatus for stabilizing the running of a web in a paper machine or a like
US6553689 *Sep 21, 2001Apr 29, 20033M Innovative Properties CompanyVapor collection method and apparatus
US6560893 *Sep 2, 1999May 13, 2003Sharon F. BakalarMethod and apparatus for heat treating webs
US6694639 *Jun 6, 2002Feb 24, 2004Tokushu Paper Mfg. Co., Ltd.Sheet material and method and apparatus for drying therefor
US7189307 *Sep 2, 2003Mar 13, 2007Kimberly-Clark Worldwide, Inc.Fibrous sheet such as paper towel with topically applied crosslinked binder of an epoxy-functional polymer such as an epichlorohydrin-methyldiallylamine copolymer and a carboxylated ethylene-vinyl acetate copolymer; improved strength; formaldehyde-free curing
US7229529 *Jul 15, 2004Jun 12, 2007Kimberly-Clark Worldwide, Inc.Low odor binders curable at room temperature
US7297231 *Jul 15, 2004Nov 20, 2007Kimberly-Clark Worldwide, Inc.Topically-applied network of a cured product of a carboxylated vinyl acetate-ethylene terpolymer, an azetidinium-functional cross-linking polymer such as polyamide-polyamine-epichlorohydrin resin, and a reactive multi-functional aldehyde; useful for the commercial production of paper towels
US7566381 *Apr 16, 2007Jul 28, 2009Kimberly-Clark Worldwide, Inc.Low odor binders curable at room temperature
US7678228 *Sep 17, 2007Mar 16, 2010Kimberly-Clark Worldwide, Inc.Binders curable at room temperature with low blocking
US7891973 *Feb 21, 2005Feb 22, 2011Nv Bekaert SaAppliance for connecting a gas-heated radiant element
US7918038 *Mar 2, 2006Apr 5, 20113M Innovative Properties CompanyVapor collection method and apparatus
US7918040 *Feb 21, 2005Apr 5, 2011Nv Bekaert SaDrier installation for drying web
US7926200 *Feb 21, 2005Apr 19, 2011Nv Bekaert SaInfrared drier installation for passing web
US7971370 *Apr 11, 2006Jul 5, 20113M Innovative Properties CompanyVapor collection method and apparatus
US20020095818 *Sep 21, 2001Jul 25, 2002Jain Nirmal K.Vapor collection method and apparatus
US20030019125 *Jun 6, 2002Jan 30, 2003Tokushu Paper Mfg. Co., LtdSheet material and method and apparatus for drying therefor
US20030230003 *Apr 23, 2003Dec 18, 20033M Innovative Properties CompanyVapor collection method and apparatus
US20040231685 *Sep 17, 2003Nov 25, 2004Pankaj Patelwrapping material for making a smoking article; comprises a substrate having bands of coating layers deposited in a pattern; for reduced ignition propensity cigarette
US20040238136 *May 16, 2003Dec 2, 2004Pankaj PatelMaterials and methods for manufacturing cigarettes
US20050000113 *Jul 11, 2003Jan 6, 2005Helge FreibergTextile machine with recirculating air heating effected by gas-heated head exchangers
US20050045294 *Sep 2, 2003Mar 3, 2005Goulet Mike ThomasLow odor binders curable at room temperature
US20050045295 *Jul 15, 2004Mar 3, 2005Kimberly-Clark Worldwide, Inc.Low odor binders curable at room temperature
US20050076929 *Oct 9, 2003Apr 14, 2005John FitzgeraldMaterials, equipment and methods for manufacturing cigarettes
US20060179680 *Apr 11, 2006Aug 17, 20063M Innovative Properties CompanyVapor collection method and apparatus
US20060191160 *Mar 2, 2006Aug 31, 20063M Innovative Properties CompanyVapor collection method and apparatus
US20070187056 *Apr 16, 2007Aug 16, 2007Goulet Mike Tincreasing wet strength to soft, absorbent paper sheets by curing an epoxy-functional polymer (epichlorohydrin-methyldiallylamine copolymer) and an epoxy-reactive polymer such as a carboxylated ethylene-vinyl acetate copolymer; formaldehyde-free curing; paper towels
US20070193060 *Feb 21, 2005Aug 23, 2007Nv Bekaert SaInfrared drier installation for passing web
US20080006381 *Sep 17, 2007Jan 10, 2008Goulet Mike TBinders curable at room temperature with low blocking
US20080006382 *Sep 17, 2007Jan 10, 2008Goulet Mike TBinders curable at room temperature with low blocking
US20080209759 *Jan 25, 2008Sep 4, 2008Shivvers Steve DCounter flow air cooling drier with fluid heating and integrated heat recovery
US20080256818 *Feb 21, 2005Oct 23, 2008Nv Bekaert SaDrier Installation for Drying Web
US20090007453 *Jan 24, 2007Jan 8, 2009Nv Bekaert SaFlame Dryer
US20090031581 *Jan 24, 2007Feb 5, 2009Nv Bekaert SaConvective system for a dryer installation
US20100206505 *Feb 13, 2009Aug 19, 2010Dan ClarahanMethod and apparatus for drying of fibrous webs
US20110035958 *Mar 13, 2009Feb 17, 2011Klaus GissingDevice and process for drying moving webs of material
AU420345B2 Title not available
DE3148321A1 *Dec 7, 1981Aug 18, 1983Fleissner Maschf Gmbh CoDevice for heat-treating horizontally guided, web-shaped products
DE3920078A1 *Jun 20, 1989Dec 28, 1989Dreizler Walter Dipl Ing FhBurner head for a blower gas burner
DE19752562A1 *Nov 27, 1997Apr 1, 1999Voith Sulzer Papiertech PatentPaper or cardboard web drying section
DE102006058710A1 *Dec 13, 2006Jun 19, 2008Daimler AgMachine tool for processing crank webs radius transition on rod- and main bearings of crankshafts for internal combustion engine, has a processing device, which is led by two orthogonal computer numerical control machine axes
EP0126221A2 *Feb 28, 1984Nov 28, 1984Hans Dr. ViessmannForced-draught burner for heating-boiler doors
EP0326227A1 *Jan 26, 1989Aug 2, 1989Stork Contiweb B.V.A drier for a web of material
EP0346041A2 *Jun 5, 1989Dec 13, 1989W.R. Grace & Co.-Conn.Control system for air flotation dryer with a built-in afterburner
EP0346042A2 *Jun 5, 1989Dec 13, 1989W.R. Grace & Co.-Conn.Air flotation dryer with built-in afterburner
EP0869323A2 *Feb 23, 1998Oct 7, 1998Heidelberger Druckmaschinen AktiengesellschaftDryer for a web of material with recirculation of exhaust gas
EP0925880A2 *Dec 18, 1998Jun 30, 1999Illinois Tool Works Inc.Suspension mechanism for a combustion chamber fan motor of a combustion powered tool
EP0990867A2 *Aug 27, 1999Apr 5, 2000Brückner Apparatebau GmbHApparatus for the heat treatment of a web
EP1182413A1 *Jun 13, 2001Feb 27, 2002Brückner Trockentechnik GmbH & Co. KGApparatus and process for treatment of material webs
EP1515103A2 *Sep 2, 2004Mar 16, 2005Fuji Photo Film Co., Ltd.Drying apparatus
FR2771161A1 Title not available
JP2001081657A * Title not available
JP2004130506A * Title not available
JPH0239939A * Title not available
JPH0323322A * Title not available
JPH01321994A * Title not available
JPH06257061A * Title not available
JPH11239983A * Title not available
JPS59213919A * Title not available
JPS60119327A * Title not available
JPS63187017A * Title not available
WO2005085729A2Feb 21, 2005Sep 15, 2005Bekaert Sa NvDrier installation for drying web
Classifications
U.S. Classification34/613, 502/400, 34/631, 34/623, 266/84, 34/635, 162/207, 451/259, 162/290, 34/617, 73/23.41, 51/293, 502/60, 73/23.37, 266/192
International ClassificationF26B9/00
Cooperative ClassificationF26B3/305, F26B13/10, F26B13/22, D21F5/008
European ClassificationF26B13/10, F26B3/30B, F26B13/22, D21F5/00G
Legal Events
DateCodeEventDescription
Nov 26, 2008ASAssignment
Owner name: BEKAERT COMBUSTION TECHNOLOGY B.V., NETHERLANDS
Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:LENOIR, PATRICK;REEL/FRAME:021892/0886
Effective date: 20080610
Owner name: NV BEKAERT SA, BELGIUM